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Comparison of the rate of smoke generated from the combustion of biomass fuels by Dr. John Orrin
A smoke chamber has been used to measure the smoke generated from
seven different biomass fuels. These fuels are wood, peanut shells,
cardboard, chipboard, straw, hay and eucalyptus leaves. This
equipment allows a direct comparison of the smoke generated between
these seven biomass fuels. A sample of each fuel was exposed to a
radiant heat source and the amount of smoke measured with time.
Analysis of the results showed that fuels such as straw or hay
produced high levels of smoke quickly for a given mass loss. More
compact (higher density) fuels took much longer to produce the same
amount of smoke illustrating the benefit of producing fuel
briquettes. This technique could also be used to measure the smoke
generated as the composition of the fuel briquette was
varied.
Smoke has been defined as the products of burning organic materials
in which small solid and liquid particles are also dispersed[1].
For communities that rely on open or three stone fires for cooking
in poorly ventilated areas, smoke provides a threat due to its
toxicity. This often results in smoke related illness[2].
The amount of smoke generated is sensitive to a wide range of
variables such as the orientation of the fuel on the stove, the
size and geometry of the fuel, the temperature and the ventilation.
The smoke chamber however allows the fuel alone to be examined
under precisely defined and constant conditions[3].
When a fire is first started or when new fuel is introduced onto
the fire, the fuel will be subject to non flaming (that is
smouldering) combustion. If the fuel is carbon based, high levels
of smoke are produced initially due to thermal pyrolysis and
evolution of volatile matter. The combustion products with high
boiling point condense as they mix with the cooler air and this
produces a mist of minute droplets. These droplets combine together
to give larger droplets of the order of 1mm that can then deposit
on surfaces to give an oily residue[4].
When smoke is present in a room, the visibility is reduced because
light is scattered and absorbed by the smoke particles. By
measuring the visibility or optical density within the room, the
amount of smoke can be measured.
The optical density is defined as:
(O.D.) = log10 ( Io/I )
Where:
O.D. = Optical Density
Io = initial intensity of light
I = final intensity of light after passing through smoke
If 50% of the light is absorbed by the smoke particles, then:
Io =100 and I = 50 and the optical density = log10 (100/50) =
0.3.
For an optical density per path length of smoke of 0.3, the
visibility is about 4 metres5. For a smoke filled room that has
been caused by a poorly vented stove, the visibility would be much
higher than this value and the optical density lower. For example,
a visibility of 10 metres and optical density per path length of
smoke of about 0.1 might be typical values.
[top]
[end]Equipment
Used For The Measurement Of Smoke
Figure 1. The Smoke Chamber used for the
Measurement of Smoke
|
Figure 2. Diagram of Smoke Chamber used for
the Measurement of Smoke
|
The smoke chamber is shown in Fig. 1. The smoke chamber has a fixed
volume of 914mm x 610mm x 914mm. As shown in Fig. 2, the smoke
chamber contains the biomass sample with holder situated on guide
rails, a light source, a photo multiplier unit and a 25 kW per m2
radiant heat source.
The sample of biomass fuel is first placed in a sample holder and
the sample holder plus biomass fuel is weighed on a digital balance
to three decimal places. The sample holder is then placed on the
guide rails away from the radiant heat source. The door of the
smoke chamber is shut and the software programme that controls the
smoke chamber is started. The photo multiplier unit is calibrated
so that 100% of the light passes across the smoke chamber
(corresponding to no smoke). Drawing the biomass sample in front of
the heat source then starts the test. As smoke is produced, the
amount of light reaching the photo multiplier unit is reduced and
the computer continuously records the results. When the light
reaching the photo multiplier tube has been reduced by 30%, the
test is stopped and the sample removed from the smoke chamber. The
sample plus sample holder is again weighed and the amount of
biomass fuel used is calculated. The test is then repeated for the
next fuel.
[top]
[end]Results
and Discussion
Figure 3. Reduction of Light Intensity with
Time (T70 = time at the end of the test)
|
. 3 shows the reduction of light intensity with time for a typical
biomass fuel. At the start of the test, little smoke is produced.
This simulates the situation when fuel is first introduced onto a
fire and the temperature of the sample is low. After a short
initial period, there is a rapid increase in the smoke produced as
the fuel sample temperature increases. The time for a 30% reduction
in light intensity was measured for all the fuel samples and the
results are shown in Fig. 4. The weight reduction and initial bulk
densities are calculated for all the fuel samples and the results
are shown in Fig. 4 and Fig. 5.
Figure 4. Results showing the time for the
smoke chamber to fill with smoke for different fuels (for 70%
transmission of light).
|
Figure 5. Bulk Density and Average Rate of
Mass Loss for Different Biomass Fuels
|
It was found that all the biomass fuels tested fall into one of
three groups.
- Group 1: This group included straw, hay, peanut shells and dry
cardboard. All these biomass fuels produced smoke quickly (in the
range 64 seconds to 93 seconds). These fuels had the lowest bulk
density (ranging from 1.28 x 10-4 g/mm3 to 1.78 x 10-4 g/mm3 ).
This group of fuels also had the highest rate of weight loss
(ranging from 0.011 g/s to 0.022 g/s). With the exception of dry
cardboard, these fuels had the highest surface area to volume ratio
exposed to the radiant heat source.
- Group 2: This group comprised wood (pine) and chipboard. These
two fuels took much longer to produce the same quantity of smoke
that caused a light reduction of 30%. The time for wood (pine) was
found to be 317 seconds and for chipboard 250 seconds. Therefore
the time required to produce smoke for a given mass loss was in the
region of 3 times longer than for group 1 fuels. As can be seen in
Fig. 5, the initial bulk density of group 2 fuels is 4 to 7 times
higher than for group 1 fuels.
- Group 3: In this group, Eucalyptus leaves and wet cardboard
both contained a large quantity of water per unit mass. As the fuel
was exposed to the radiant heat source, large quantities of steam
(not smoke) were produced and the time to produce smoke was
therefore much longer than the other groups of fuels.
Fig. 6 shows the relationship between the average rate of mass loss
of the biomass fuel and the time to produce smoke. Group 1 fuels
produced smoke quickly with cardboard producing almost twice the
same amount of smoke for a given mass loss as peanut shells. Group
2 fuels took much longer to produce smoke but had a much lower
average rate of mass loss. Group 3 fuels (cardboard (wet) and
Eucalyptus leaves) were outside the curve shown in Fig. 6 due to
the high water content of these biomass fuels.
Figure 6. Time to Produce Smoke (70%
Transmission of Light) against Rate of Mass Loss
|
The time required to produce a fixed quantity of smoke has been
measured for a number of different biomass fuels. Each biomass fuel
has been subject to the same radiant heat source and the same
radiant intensity. This simulated the conditions whereby a fuel is
first introduced onto a fire and produces smoke by non flaming
(smouldering) combustion. The fuels were broadly classified into
three groups. The first group (straw, hay, peanut shells and dry
cardboard) had a low bulk density and would produce a large amount
of smoke quickly if allowed to smoulder on an open fire. The second
group (wood and chipboard) took much longer to produce the same
amount of smoke for a given mass loss. The third group (wet
cardboard and air dried Eucalyptus leaves) contained large amounts
of water and took very much longer to produce a given amount of
smoke again for a given mass loss. This last group would have
produced large quantities of water vapour (not smoke) for a given
mass loss. The results indicate the benefits of making briquettes
of the fuel. Samples of briquettes could be tested using this
equipment and the composition of the briquette varied to find the
minimum rate of smoke production under non flaming (smouldering)
conditions.
[top]
[end]Notes
and References
- Gross, D., Loftus, J.J., and Robertson, A.F. (1967). “Method
for measuring smoke from burning materials.” Symposium on “Fire
Test Methods – Restraint and Smoke”. 1966, ASTM STP 422 (ed A.F.
Robertson), pp.166-204. American Society for Testing and Materials,
Philadelphia.
- www.itdg.org/html/smoke/smoke_report.htm
- www.firetestingtechnology.co.uk
- “An Introduction to Fire Dynamics”. Dougal Drysdale. 1990. ISBN
0 471 90613 1.
- “Generation of Heat and Chemical Compounds in Fires” Archibald
Tewarson. SFPE Handbook of Fire Protection Engineering, 1988,
Section 1/Chapter13 p.1-194.
[top]
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the original article
Comparison of the
rate of smoke generated from the combustion of different biomass
fuels by Dr. John Orrin (526 KB)
[top]
[end]Contents:
Boiling Point 54 - Climate change and household energy
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cooking – time to grasp the opportunity -
BP54:Health and Greenhouse Gas Impacts in
Africa -
BP54:Carbon Finance for Healthy Kitchens -
BP54:Critique of GHG stove assessment
methods -
BP54: Practical Action CO2 offsetting
experience -
BP54: Credible Carbon Offsets for African
Households -
BP54: GTZ News -
BP54: Practical Action News -
BP54: Marine conservation and energy efficient
stoves -
BP54: Can Carbon Finance Clean Cooking? -
BP54: Rates of smoke emissions -
BP54: A Polyethylene Dome for Biogas Plants
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BP54: HEDON news
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